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FR2632873A1 - INTERNAL MIXER WITH IMPROVED ROTORS - Google Patents

INTERNAL MIXER WITH IMPROVED ROTORS Download PDF

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Publication number
FR2632873A1
FR2632873A1 FR8808205A FR8808205A FR2632873A1 FR 2632873 A1 FR2632873 A1 FR 2632873A1 FR 8808205 A FR8808205 A FR 8808205A FR 8808205 A FR8808205 A FR 8808205A FR 2632873 A1 FR2632873 A1 FR 2632873A1
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FR
France
Prior art keywords
passage
profile
rotor
chamber
curvature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
FR8808205A
Other languages
French (fr)
Other versions
FR2632873B1 (en
Inventor
Dominique Simonet
Simonet Dominique
Michel Garmy
Garmy Michel
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Compagnie Generale des Etablissements Michelin SCA
Original Assignee
Compagnie Generale des Etablissements Michelin SCA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to FR8808205A priority Critical patent/FR2632873B1/en
Application filed by Compagnie Generale des Etablissements Michelin SCA filed Critical Compagnie Generale des Etablissements Michelin SCA
Priority to ES198989109767T priority patent/ES2035429T3/en
Priority to AT89109767T priority patent/ATE81051T1/en
Priority to EP89109767A priority patent/EP0346680B1/en
Priority to DE8989109767T priority patent/DE68903047T2/en
Priority to US07/361,353 priority patent/US4917501A/en
Priority to JP1153550A priority patent/JPH0755498B2/en
Publication of FR2632873A1 publication Critical patent/FR2632873A1/en
Application granted granted Critical
Publication of FR2632873B1 publication Critical patent/FR2632873B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • B29B7/186Rotors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/82Heating or cooling
    • B29B7/826Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495Systems, i.e. flow charts or diagrams; Plants for mixing rubber

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The rotor (1) for internal mixing comprises blades (10) whose profile ensures adequate stressing of the rubber between the blade (10) and the internal wall of the chamber (2). This profile comprises, successively, a progressively converging region (23), a passage at the tip (21), a progressively diverging region (24), then a zone breaking the continuity of the profile, called a detachment (22), followed by an accentuated diverging region (25).

Description

- 1 - 3- 1 - 3

MELANGEUR INTERNE A ROTORS PERFECTIONNES  INTERNAL MIXER WITH IMPROVED ROTORS

La présente invention se rapporte aux mélangeurs internes.  The present invention relates to internal mixers.

Plus particulièrement elle concerne la définition du profil  More particularly it concerns the definition of the profile

des ailes dont sont pourvus ces rotors.  wings with which these rotors are provided.

Les mélangeurs internes sont des malaxeurs à marche discontinue convenant pour la préparation du caoutchouc et d'autres matières plastiques. Ils comportent une cuve fermée à une ou deux chambres cylindriques communicant entre elles, chaque chambre comportant un rotor.Chaque rotor comporte une ou plusieurs ailes. On caractérise le rotor par son profil (section par un plan perpendiculaire à l'axe de rotation donnant notamment le profil des ailes) et par son diagramme qui est un développement à plat sur un plan parallèle à l'axe de rotation, donnant le positionnement des ailes à la surface du rotor, notamment la position, l'orientation par rapport aux bords, et l'étendue de la zone d'écart minimum entre la paroi de la chambre et la surface  The internal mixers are batch mixers suitable for the preparation of rubber and other plastics. They have a closed vessel with one or two cylindrical chambers communicating with each other, each chamber comprising a rotor. Each rotor comprises one or more wings. The rotor is characterized by its profile (section by a plane perpendicular to the axis of rotation giving in particular the profile of the wings) and by its diagram which is a flat development on a plane parallel to the axis of rotation, giving the positioning wings on the surface of the rotor, in particular the position, the orientation with respect to the edges, and the extent of the zone of minimum distance between the wall of the chamber and the surface

du rotor (zone appelée dans la suite "passage au fin").  of the rotor (hereinafter called "passage to the end").

Le choix et la combinaison du nombre de chambres et du type de rotor dépendent de la composition des mélanges de caoutchouc ou matières plastiques à réaliser. Les mélangeurs internes les plus répandus pour la préparation du caoutchouc non vulcanisé comportent deux chambres et deux rotors non engrenants, tournant en sens opposés à des vitesses différentes. On en voit un exemple dans le brevet  The choice and combination of the number of chambers and the type of rotor depends on the composition of the rubber or plastic mixtures to be produced. The most common internal mixers for the preparation of unvulcanized rubber have two chambers and two non-meshed rotors, rotating in opposite directions at different speeds. We see an example in the patent

US 4 456 381.US 4,456,381.

Le but recherché dans les mélangeurs internes est de forcer les constituants du mélange à passer d'une chambre à l'autre et, à l'intérieur d'une chambre, d'un côté à l'autre, dans le sens axial de celle-ci, et aussi à forcer le mélange à  The aim sought in internal mixers is to force the constituents of the mixture to pass from one chamber to another and, inside a chamber, from one side to the other, in the axial direction of that and also to force the mixture to

passer entre les pales des rotors et les parois 'de la cuve.  pass between the rotor blades and the walls of the tank.

Ceci permet de réaliser une macro dispersion des constituants et une micro dispersion des additifs. La macro dispersion est plutôt le fait du transfert de masse de -2- matière entre les chambres de la cuve et des transferts axiaux, c'est-à-dire le long des ailes du rotor dans chacune des chambres, alors que la micro dispersion est plutôt conditionnée par le passage entre l'aile et la paroi de la chambre. Les rotors de mélangeurs internes ont l'inconvénient de présenter, dans la partie de passage au fin, une zone de travail intense de longueur courte, qui sollicite les matériaux de manière brutale et irrégulière, pouvant provoquer des glissements importants ainsi que pour certains élastomères des décohésions accompagnées d'un mauvais état de mélangeage. La figure 1 est une vue d'un profil d'aile de rotor 1 selon lart antérieur. En particulier, on remarque la présence d'arêtes vives 20 qui délimitent de part et d'autre la zone de passage au fin 21. On définit le côté avant du passage au fin 21 en quittant celui-ci dans le sens de rotation du rotor 1 (flèche 11) qui correspond donc au convergent matérialisé par la surface de l'aile en coopération avec la paroi de la chambre 2. A l'inverse, le  This allows a macro dispersion of the constituents and a micro dispersion of the additives. Macro dispersion is rather the result of the mass transfer of -2- material between the chambers of the tank and axial transfers, that is to say along the wings of the rotor in each of the chambers, while micro dispersion is rather conditioned by the passage between the wing and the wall of the chamber. The rotors of internal mixers have the disadvantage of having, in the passage portion at the end, an intense working area of short length, which stresses the materials in a brutal and irregular manner, which can cause significant slippage as well as for certain elastomers of the decohesions accompanied by a poor state of mixing. Figure 1 is a view of a rotor wing profile 1 according to the prior art. In particular, we note the presence of sharp edges 20 which delimit on both sides the passage zone at the end 21. The front side of the passage at the end 21 is defined by leaving it in the direction of rotation of the rotor. 1 (arrow 11) which therefore corresponds to the convergent materialized by the surface of the wing in cooperation with the wall of the chamber 2. Conversely, the

côté arrière est situé du côté opposé par rapport au sens de-  rear side is located on the opposite side from the direction of-

rotation. On remarque également que, en arrière du passage au fin 21, on a un accroissement brutal et important de  rotation. We also note that, behind the passage at the end 21, there is a sudden and significant increase in

l'écart entre l'aile 10 et la paroi de la chambre 2.  the distance between the wing 10 and the wall of the chamber 2.

D'autre part les mélangeurs internes connus ne peuvent assurer une bonne maitrise des échanges thermiques lors du  On the other hand, the known internal mixers cannot ensure good control of the heat exchanges during the

cycle de mélangeage.mixing cycle.

Le but de la présente invention est d'améliorer la micro dispersion obtenue par l'action d'un mélangeur interne, en proposant une nouvelle conception du profil d'une aile de mélangeur interne. Un autre objectif de l'invention consiste à améliorer la capacité d'une aile ainsi optimisée à évacuer les calories dégagées par l'opération de mélangeage. Selon l'invention, le mélangeur interne comportant une cuve de mélangeage constituée par au moins une chambre cylindrique dans laquelle tourne un rotor, ledit rotor comportant au moins deux ailes inclinées en sens opposés, le -3- profil de l'aile définissant avec la paroi de la chambre un convergent puis un divergent, séparés par un passage au fin, est caractérisé en ce que, de part et d'autre du passage au fin, la courbure du profil est sensiblement constante, et en ce que, écarté du passage au fin dans le sens opposé au sens de rotation de l'aile, le profil comporte un décrochement, suivi toujours-dans le sens opposé au sens de rotation, d'un second divergent plus accentué que le divergent compris entre le passage au fin et le décrochement. Un rotor de mélangeur interne perfectionné suivant l'invention est remarquable par le fait qu'il n'existe pas d'arêtes vives dans la partie de passage au fin o se produit la sollicitation la plus intense. En effet la partie- convergente a un profil convexe. Ce profil est sensiblement conservé dans le passage au fin et après celui-ci. Donc le début du divergent, juste en arrière du passage au fin, est très progressif. Il y a un relâchement lent et progressif de la sollicitation au delà du passage au fin, contrairement à la technique antérieure o le passage au fin marque également la rupture de la continuité du profil. Les' profils des ailes des rotors connus présentent donc un convergent, parfois progressif, un passage au fin, puis un divergent important. Le profil proposé par la présente invention présente successivement un convergent progressif, un passage au fin, un divergent progressif, puis une zone de rupture de la continuité du profil, appelée  The object of the present invention is to improve the micro dispersion obtained by the action of an internal mixer, by proposing a new design of the profile of an internal mixer wing. Another objective of the invention consists in improving the capacity of a wing thus optimized to evacuate the calories released by the mixing operation. According to the invention, the internal mixer comprising a mixing tank constituted by at least one cylindrical chamber in which a rotor rotates, said rotor comprising at least two wings inclined in opposite directions, the profile of the wing defining with the wall of the chamber a convergent then a divergent, separated by a passage at the end, is characterized in that, on either side of the passage at the end, the curvature of the profile is substantially constant, and in that, spaced from the passage at the end in the direction opposite to the direction of rotation of the wing, the profile comprises an offset, always followed in the direction opposite to the direction of rotation, of a second divergence more accentuated than the divergence comprised between the passage at the end and the dropout. An improved internal mixer rotor according to the invention is remarkable in that there are no sharp edges in the passage part at the end where the most intense stress occurs. Indeed, the converging part has a convex profile. This profile is substantially preserved in the passage at the end and after it. So the beginning of the divergent, just behind the passage at the end, is very progressive. There is a slow and progressive relaxation of the stress beyond the passage at the end, unlike the prior art where the passage at the end also marks the rupture of the continuity of the profile. The 'profiles of the wings of known rotors therefore have a convergent, sometimes progressive, a passage at the end, then a significant divergence. The profile proposed by the present invention successively presents a progressive convergent, a passage at the end, a progressive divergent, then a zone of rupture of the continuity of the profile, called

décrochement, suivie d'un divergent accentué.  drop, followed by an accentuated divergence.

La consultation dés figures suivantes permet de bien  The consultation of the following figures makes it possible

comprendre l'invention.understand the invention.

La figure 2 montre le profil d'une aile selon l'invention.  Figure 2 shows the profile of a wing according to the invention.

La figure 3 montre un diagramme d'un rotor de mélangeur  Figure 3 shows a diagram of a mixer rotor

interne.-internal.-

Les figures 4 et 5 illustrent le refroidissement d'une aile  Figures 4 and 5 illustrate the cooling of a wing

selon l'invention.according to the invention.

Pour rappel, la figure 1 illustre l'art antérieur.  As a reminder, Figure 1 illustrates the prior art.

A la figure 2, on aperçoit un rotor 1, une aile 10, et la paroi de la chambre 2 dans laquelle le rotor se trouve  In FIG. 2, we can see a rotor 1, a wing 10, and the wall of the chamber 2 in which the rotor is located.

26328-326328-3

-4- disposé. L'aile 10 définit, avec la paroi de la chambre 2, un convergent 23 puis un passage au fin 21. Il y a une distance très nette entre le passage au fin 21 et la zone dite de décrochement 22, séparant un premier divergent 24  -4- arranged. The wing 10 defines, with the wall of the chamber 2, a convergent 23 then a passage at the end 21. There is a very clear distance between the passage at the end 21 and the so-called recess zone 22, separating a first diverging point 24

progressif, d'un second divergent 25 très accentué.  progressive, from a very divergent second divergent 25.

Le convergent Z3 du profil est défini dans un plan perpendiculaire à l'axe du rotor par un centre C et un rayon de courbure R. Le rayon de courbure est constant le long de l'aile. Le centre de courbure C est tel que sa distance à l'axe du rotor O est comprise entre des valeurs 0,1 Ro et 0,6 Ro o Ro est le rayon de la cuve. Le rayon de courbure R est lui compris entre les valeurs 0,4 Ro et 0,7 Ro. Le passage au fin 21 est défini dans un plan perpendiculaire à l'axe par le point A de distance maximale à l'axe du rotor,  The convergent Z3 of the profile is defined in a plane perpendicular to the axis of the rotor by a center C and a radius of curvature R. The radius of curvature is constant along the wing. The center of curvature C is such that its distance from the axis of the rotor O is between values 0.1 Ro and 0.6 Ro o Ro is the radius of the tank. The radius of curvature R is between the values 0.4 Ro and 0.7 Ro. The passage at the end 21 is defined in a plane perpendicular to the axis by the point A of maximum distance from the axis of the rotor,

autrement dit d'écart minimal avec la paroi de la chambre 2.  in other words a minimum distance from the wall of chamber 2.

Le divergent 24 juste après le passage au fin 21 comporte un profil conçu de la même façon (rayon de courbure choisi dans le même intervalle). Le point B qui est la trace d'une arête vive, matérialise dans cet exemple le décrochement 22 et est situé à une distance huit fois supérieure au jeu entre le point A et la paroi de la chambre. Ces caractéristiques géométriques ont été déterminées de façon expérimentale et permettent de réaliser, en adoptant le diagramme représenté à la figure 3, d'excellentes  The divergent 24 just after the passage at the end 21 has a profile designed in the same way (radius of curvature chosen in the same interval). Point B which is the trace of a sharp edge, materializes in this example the recess 22 and is located at a distance eight times greater than the clearance between point A and the wall of the chamber. These geometric characteristics have been determined experimentally and make it possible to achieve, by adopting the diagram shown in Figure 3, excellent

performances de macro dispersion et de micro dispersion.  macro dispersion and micro dispersion performances.

Sur ce diagramme, on voit que l'on dispose deux ailes 10 s'étendant dans la direction axiale sur une longueur comprise entre 0.6 Lo et 0.8 Lo, o Lo est la longueur du rotor 1. Les ailes 10 sont inclinées d'un angle compris  In this diagram, it can be seen that there are two wings 10 extending in the axial direction over a length of between 0.6 Lo and 0.8 Lo, where Lo is the length of the rotor 1. The wings 10 are inclined at an angle including

entre 15' et 30'.between 15 'and 30'.

Un tel profil permet une sollicitation progressive du matériau entre la paroi de la chambre et le rotor à chaque passage de la matière. Il n'existe plus de sollicitations brutales. Il permet aussi un accompagnement de la matière après le passage au fin qui permet une relaxation du matériau. Un tel profil permet de plus une bonne microdispersion des charges renforçantes. Grâce à cette solution, on évite les décohésions du matériau amenées par des glissements importants à la paroi, observées dans l'art - 5 - antérieur, ce qui permet d'obtenir un meilleur état final de mélangeage. Enfin un rotor 1 de mélangeur interne perfectionné suivant l'invention comporte une chambre 12 de refroidissement localisée de préférence et principalement sous le convergent 23 dans la zone o se produisent les dégagements de chaleur les plus intenses (figure 4 et 5). La totalité du débit de réfrigérant est utilisée pour obtenir un échange thermique optimal, les chambres de refroidissement étant en série, comme cela apparaîlt à la figure 5. Le rotor 1 suivant l'invention offre une résistance mécanique suffisante pour l'installation de telles chambres dans les zones de travail  Such a profile allows progressive loading of the material between the wall of the chamber and the rotor at each passage of the material. There are no longer any brutal requests. It also allows support for the material after the passage at the end which allows relaxation of the material. Such a profile also allows good microdispersion of reinforcing fillers. Thanks to this solution, the decohesions of the material brought about by significant slippages to the wall, observed in the prior art, are avoided, which makes it possible to obtain a better final state of mixing. Finally, a rotor 1 of an improved internal mixer according to the invention comprises a cooling chamber 12 preferably located and mainly under the convergent 23 in the zone where the most intense heat releases occur (FIGS. 4 and 5). The entire refrigerant flow is used to obtain optimal heat exchange, the cooling chambers being in series, as shown in FIG. 5. The rotor 1 according to the invention offers sufficient mechanical strength for the installation of such chambers in work areas

intense du matériau.intense material.

Il est bien clair que différentes modifications peuvent être apportées aux ailes de mélangeurs internes sans sortir du cadre de la présente invention chaque fois que l'on en reproduira les caractéristiques essentielles portant sur le  It is quite clear that various modifications can be made to the wings of internal mixers without departing from the scope of the present invention each time the essential characteristics relating to it are reproduced.

profil de l'aile 10.wing profile 10.

-6--6-

Claims (4)

REVENDICATIONS 1. Mélangeur interne comportant une cuve de mélangeage constituée par au moins une chambre cylindrique dans laquelle tourne un rotor (1), ledit rotor (1) comportant au moins deux ailes (10) inclinées en sens opposés, le profil de l'aile définissant avec la paroi de la chambre (2) un convergent (23) puis un divergent (24), séparés par un passage au fin (21) , caractérisé en ce que, de part et d'autre du passage au fin (21), la courbure du profil est sensiblement constante, et en ce que, écarté du passage au fin (21) dans le sens opposé au sens de rotation de l'aile, le profil comporte un décrochement (22) suivi, toujours dans le sens opposé au sens de rotation, d'un second divergent plus accentué (25) que le divergent (24) compris entre le passage au fin (21)  1. Internal mixer comprising a mixing tank constituted by at least one cylindrical chamber in which a rotor (1) rotates, said rotor (1) comprising at least two wings (10) inclined in opposite directions, the profile of the wing defining with the wall of the chamber (2) a convergent (23) then a divergent (24), separated by a passage at the end (21), characterized in that, on either side of the passage at the end (21), the curvature of the profile is substantially constant, and in that, separated from the passage at the end (21) in the direction opposite to the direction of rotation of the wing, the profile comprises a recess (22) followed, always in the direction opposite to the direction of rotation, of a second more marked divergence (25) than the divergence (24) between the passage at the end (21) et le décrochement (22).and the offset (22). 2. Mélangeur interne selon la revendication 1, caractérisé en ce que la courbure sensiblement constante de part et d'autre du passage au fin (21) respecte les relations suivantes: 0.1 Ro < OC < 0.6 Ro 0.4 Ro < R < 0.7 Ro o Ro est le rayon de courbure de la chambre (2) de mélangeage O est le centre de la chambre (2) de mélangeage R est le rayon de courbure du profil  2. Internal mixer according to claim 1, characterized in that the curvature substantially constant on either side of the passage at the end (21) respects the following relationships: 0.1 Ro <OC <0.6 Ro 0.4 Ro <R <0.7 Ro o Ro is the radius of curvature of the mixing chamber (2) O is the center of the mixing chamber (2) R is the radius of curvature of the profile C est le centre de courbure du profil.  It is the center of curvature of the profile. 3. Mélangeur interne selon l'une des revendications 1 ou 2,  3. Internal mixer according to one of claims 1 or 2, caractérisé en ce que la distance séparant ledit décrochement (22) du passage au fin (21) est supérieure à huit fois l'intervalle compris entre le rotor (1) et la  characterized in that the distance separating said recess (22) from the passage at the end (21) is greater than eight times the interval between the rotor (1) and the paroi de la chambre (2)'au droit du passage su fin (21).  wall of the chamber (2) 'at the right end passage (21). 4. Mélangeur interne selon l'une des revendications 1 à 3,  4. Internal mixer according to one of claims 1 to 3, caractérisé en ce que chaque rotor (1) comporte des moyens -7- de refroidissement internes principalement disposés sous  characterized in that each rotor (1) comprises internal cooling means -7- mainly arranged under le convergent (23).the convergent (23).
FR8808205A 1988-06-16 1988-06-16 INTERNAL MIXER WITH IMPROVED ROTORS Expired - Fee Related FR2632873B1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
FR8808205A FR2632873B1 (en) 1988-06-16 1988-06-16 INTERNAL MIXER WITH IMPROVED ROTORS
AT89109767T ATE81051T1 (en) 1988-06-16 1989-05-30 INTERNAL MIXER WITH IMPROVED ROTORS.
EP89109767A EP0346680B1 (en) 1988-06-16 1989-05-30 Internal mixer with modified rotors
DE8989109767T DE68903047T2 (en) 1988-06-16 1989-05-30 INTERNAL MIXER WITH IMPROVED ROTORS.
ES198989109767T ES2035429T3 (en) 1988-06-16 1989-05-30 INTERNAL MIXER WITH PERFECTED ROTORS.
US07/361,353 US4917501A (en) 1988-06-16 1989-06-05 Internal mixer with improved rotors
JP1153550A JPH0755498B2 (en) 1988-06-16 1989-06-15 Closed mixer with improved impeller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR8808205A FR2632873B1 (en) 1988-06-16 1988-06-16 INTERNAL MIXER WITH IMPROVED ROTORS

Publications (2)

Publication Number Publication Date
FR2632873A1 true FR2632873A1 (en) 1989-12-22
FR2632873B1 FR2632873B1 (en) 1990-09-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
FR8808205A Expired - Fee Related FR2632873B1 (en) 1988-06-16 1988-06-16 INTERNAL MIXER WITH IMPROVED ROTORS

Country Status (7)

Country Link
US (1) US4917501A (en)
EP (1) EP0346680B1 (en)
JP (1) JPH0755498B2 (en)
AT (1) ATE81051T1 (en)
DE (1) DE68903047T2 (en)
ES (1) ES2035429T3 (en)
FR (1) FR2632873B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019224466A1 (en) 2018-05-24 2019-11-28 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and means for attaching same
WO2021018521A1 (en) 2019-08-01 2021-02-04 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and fixation system

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ATE300406T1 (en) * 1999-04-16 2005-08-15 Cabot Corp METHOD AND DEVICE FOR PRODUCING AND TREATING ELASTOMERIC COMPOSITE MATERIALS, AND ELASTOMERIC COMPOSITE MATERIAL THAT CAN BE PRODUCED BY THE METHOD
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Cited By (4)

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Publication number Priority date Publication date Assignee Title
WO2019224466A1 (en) 2018-05-24 2019-11-28 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and means for attaching same
US11478955B2 (en) 2018-05-24 2022-10-25 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and means for attaching same
WO2021018521A1 (en) 2019-08-01 2021-02-04 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and fixation system
US12296505B2 (en) 2019-08-01 2025-05-13 Compagnie Generale Des Etablissements Michelin Rotor with anti-wear device and fixation system

Also Published As

Publication number Publication date
ES2035429T3 (en) 1993-04-16
US4917501A (en) 1990-04-17
EP0346680A1 (en) 1989-12-20
DE68903047D1 (en) 1992-11-05
FR2632873B1 (en) 1990-09-28
EP0346680B1 (en) 1992-09-30
ATE81051T1 (en) 1992-10-15
JPH0232812A (en) 1990-02-02
DE68903047T2 (en) 1993-02-18
JPH0755498B2 (en) 1995-06-14

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